CN107438658B

CN107438658B - Free-flowing solid particulate laundry detergent composition

Info

Publication number: CN107438658B
Application number: CN201680020201.5A
Authority: CN
Inventors: A·切费; J·R·多根; A·麦克米金; A·T·布鲁克; C·皮克林; P·A·戈德; W·A·考菲尔德
Original assignee: Procter and Gamble Co
Current assignee: Procter and Gamble Co
Priority date: 2015-03-30
Filing date: 2016-03-30
Publication date: 2020-04-21
Anticipated expiration: 2036-03-30
Also published as: ZA201705800B; US9951301B2; CN107438658A; EP3075828A1; WO2016160866A1; EP3075828B1; US20160289607A1

Abstract

The present invention relates to a free-flowing solid particulate laundry detergent composition comprising: (a)0.1 to 5 wt% of toner particles comprising: (i)2 to 10 weight percent of a toner, wherein the toner has the following structure:

Description

Free-flowing solid particulate laundry detergent composition

Technical Field

The present invention relates to a free-flowing solid particulate laundry detergent composition. The composition of the present invention comprises toner particles and AES particles. The compositions of the present invention, while exhibiting excellent tinting performance and excellent surfactant performance, also minimize undesirable over-tinting negatives.

Background

Laundry detergent powder manufacturers seek to provide products with excellent whiteness and soil cleaning performance. To meet this demand, laundry detergent powder manufacturers incorporate into their products ingredients such as hueing agents and detersive surfactants. There are many different types of hueing agents and surfactants available to laundry detergent manufacturers, and there are many different ways in which these ingredients can be incorporated into laundry detergent powder products. It is particularly noted that when incorporating hueing agents into laundry detergent powder products, excellent hueing performance should be ensured, but undesirable over-hueing negatives are minimized.

The inventors have found that the whiteness and soil cleaning performance caused by laundry detergent powders depends not only on the combination of the type of toner and the type of detersive surfactant incorporated, but also on the particle architecture of the toner particles and the detersive surfactant particles.

The inventors have found that the whiteness and soil cleaning performance of a laundry detergent powder product is improved when the particle architecture is optimised as defined in the claims of the present invention. Furthermore, the inventors have found that this particular particle architecture also minimizes undesirable over-toning negative conditions.

Disclosure of Invention

wherein:

r1 and R2 are independently selected from: h; an alkyl group; an alkoxy group; an alkylene oxide; an alkyl terminated alkylene oxide; urea; and an amide group;

r3 is a substituted aryl group;

x is a substituent comprising a sulfonamide moiety and optionally an alkyl and/or aryl moiety, and wherein the substituent comprises at least one alkyleneoxy chain comprising an average molar distribution of at least four alkyleneoxy moieties; and

(ii)60 to 98 weight percent of a clay; and (b)0.5 to 20% by weight of AES particles comprising: (i) from 40 wt% to 60 wt% of a partially ethoxylated alkyl sulphate anionic detersive surfactant, wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has an average molar ethoxylation degree of from 0.8 to 1.2, and wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has a molar ethoxylation distribution such that: (i.i)40 to 50 wt% are unethoxylated, having a degree of ethoxylation of 0; (i.ii)20 to 30 wt% have a degree of ethoxylation of 1; (i.iii)20 to 40 wt% have a degree of ethoxylation of 2 or more; (ii)20 to 50 wt% of a salt, wherein the salt is selected from sulphate and/or carbonate; and (iii)10 to 30 weight percent silica.

Detailed Description

Free-flowing solid particulate laundry detergent composition: a free-flowing solid particulate laundry detergent composition comprises from 0.1 wt% to 5 wt%, preferably from 0.1 wt% to 2 wt% of a hueing agent particle and from 0.5 wt% to 20 wt%, preferably from 1 wt% to 10 wt% or even from 2 wt% to 5 wt% of an AES particle. The toner particles and AES particles are described in more detail below. The composition preferably comprises from 35 wt% to 80 wt%, from 35 wt% to 70 wt% or even from 40 wt% to 60 wt% of the spray-dried particles. Spray dried particles are described in more detail below. The composition may further comprise: 1 to 30 wt% LAS particles; 0.1 to 5 wt%, preferably 0.5 to 2 wt% of polymer particles; and/or from 0.1 to 5 wt%, preferably from 0.2 to 2 wt% of silicone particles. These particles are described in more detail below.

Preferably, the composition comprises: (a)0 wt% to 5 wt% zeolite builder; (b)0 wt% to 5 wt% phosphate builder; and (c)0 to 5 wt% sodium carbonate.

Preferably, the composition comprises alkylbenzene sulphonate and ethoxylated alkyl sulphate in a weight ratio of from 5:1 to 20: 1.

Typically, the free-flowing solid particulate laundry detergent composition is a fully formulated laundry detergent composition, not a part thereof, such as a spray-dried, extruded or agglomerate particle that forms only a part of the laundry detergent composition. Typically, the solid composition comprises a plurality of chemically distinct particles, such as spray-dried and/or agglomerated and/or extruded base detergent particles in combination with one or more, typically two or more, or five or more, or even ten or more of the following particles selected from: surfactant granules, including surfactant agglomerates, surfactant extrudates, surfactant needles, surfactant noodles, surfactant flakes; phosphate particles, zeolite particles; silicate particles, especially sodium silicate particles; carbonate particles, especially sodium carbonate particles; polymer particles, such as carboxylate polymer particles, cellulosic polymer particles, starch particles, polyester particles, polyamine particles, terephthalate polymer particles, polyethylene glycol particles; aesthetic particles such as colored bars, needles, lamellar particles, and annular particles; enzyme particles, such as protease particles, amylase particles, lipase particles, cellulase particles, mannanase particles, pectate lyase particles, xyloglucanase particles, bleaching enzyme particles, and co-particles of any of these enzymes, preferably these enzyme particles comprise sodium sulfate; bleach particles, such as percarbonate particles, in particular coated percarbonate particles, such as percarbonate coated with carbonate, sulphate, silicate, borosilicate or any combination thereof, perborate particles, bleach activator particles, such as tetraacetylethylenediamine particles and/or alkylphenenesulphonate particles, bleach catalyst particles, such as transition metal catalyst particles, and/or isoquinolinium bleach catalyst particles, preformed peracid particles, in particular coated preformed peracid particles; filler particles such as sulfate and chloride particles; clay particles such as montmorillonite particles and particles of clays and silicones; flocculant particles, such as polyethylene oxide particles; wax particles, such as wax agglomerates; silicone particles, brightener particles; dye transfer inhibitor particles; dye fixative particles; perfume particles, such as perfume microcapsules and starch encapsulated perfume accord particles or pro-perfume particles, such as schiff base reaction product particles; a hueing dye particle; chelant particles, such as chelant agglomerates; and any combination thereof.

Spray-dried particles: the spray-dried particles comprise: (a) from 8% to 24% by weight of alkyl benzene sulphonate anionic detersive surfactant; (b)5 to 18 wt% of a silicate; (c) 0% by weightTo 10% by weight of sodium carbonate; and (d)0 to 5 weight percent of a carboxylate polymer.

Preferably, the spray-dried particles are free of sodium carbonate. Preferably, the spray-dried particles comprise a sulphate salt, preferably sodium sulphate. Preferably, the spray dried granules comprise 54 to 87 wt% sodium sulphate.

Preferably, the spray-dried particles comprise 5 to 18 wt% silicate, wherein SiO₂:Na₂The ratio of O is in the range of 1.6 to 2.35. It may be preferred when the silicate has a low SiO₂:Na₂An O ratio, for example of about 1.6, then the silicate content present in the spray-dried particles is high, for example about 18 wt%. It may also be preferred when the silicate has a high SiO₂:Na₂At an O ratio of, for example, about 2.35, then the silicate content present in the spray-dried particles is low, for example, about 5 wt%.

Preferably, the spray-dried particles have a bulk density of from 350g/l to 500 g/l. Typically, the spray dried particles have a weight average particle size of from 400 microns to 450 microns. Typically, the spray-dried particles have a particle size distribution such that the geometric span is from 1.8 to 2.0.

Method for making spray-dried particles: the spray-dried particles are prepared by a spray-drying process. Typically, the aqueous mixture is prepared by contacting an alkylbenzene sulphonate anionic detersive surfactant, a silicate and water. The carboxylate polymer (if present) is then added to the aqueous mixture. Typically, the sodium sulfate is then contacted with the aqueous mixture to form a crutcher mixture. Typically, the crutcher mixture comprises 26 to 32 wt% water. Typically, the crutcher mixture is then spray dried to form the spray-dried granules.

LAS particles: the LAS particle comprises: (a) from 30% to 50% by weight of an alkylbenzene sulphonate anionic detersive surfactant; and (b)50 to 70 wt% of a salt, wherein the salt is a sodium salt and/or a carbonate salt. Preferably, the LAS particle comprises1 to 5% by weight of a carboxylate polymer. The LAS particle may be an LAS agglomerate or an LAS spray dried particle. Typically, the LAS spray dried particles have a bulk density of from 300g/l to 400 g/l.

Method of making LAS particles: the LAS particle is preferably prepared by an agglomeration process or a spray drying process.

Typically, the spray drying process comprises the step of contacting the alkylbenzene sulphonate anionic detersive surfactant and water to form an aqueous mixture. Preferably, the carboxylate polymer (if present) is then contacted with the aqueous mixture. Typically, the salt is then contacted with the aqueous mixture to form a crutcher mixture. Typically, the crutcher mixture comprises at least 40 wt% water. This level of water is preferred in the crutcher, especially when the salt is sodium sulphate. This is because this amount of water promotes excellent dissolution of sodium sulfate in the crutcher mixture. Typically, the crutcher mixture is then spray dried to form the LAS spray dried granules.

Preferably, the inlet air temperature during the spray drying step is 250 ℃ or less. Controlling the inlet air temperature of the spray drying step in this manner is important because of the thermal stability of the crutcher mixture, which is due to the high organic content in the crutcher mixture.

The spray drying step may be co-current or counter-current.

AES particles: the AES particle comprises: (a) from 40 wt% to 60 wt% of a partially ethoxylated alkyl sulphate anionic detersive surfactant, wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has an average molar ethoxylation degree of from 0.8 to 1.2, and wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has a molar ethoxylation distribution such that: (i) from 40 wt% to 50 wt% are unethoxylated, having a degree of ethoxylation of 0; (ii)20 to 30 wt% have a degree of ethoxylation of 1; (iii)20 to 40 wt% has a degree of ethoxylation of 2 or greater; (b)20 to 50 wt.% ofAmount% salt, wherein the salt is selected from sulfate and/or carbonate; and (c)10 to 30 weight percent silica. Preferably, the weight ratio of partially ethoxylated alkyl sulphate anionic detersive surfactant to silica is from 1.3:1 to 6:1, preferably from 2:1 to 5: 1. Preferably, the AES particles are in the form of agglomerates.

Process for the manufacture of partially ethoxylated alkyl sulphate anionic detersive surfactants: the ethylene oxide and alkyl alcohol are reacted together to form the ethoxylated alkyl alcohol, typically with the molar ratio of ethylene oxide to alkyl alcohol used as the reaction substrate being in the range of 0.8 to 1.2, with the stoichiometric ratio (1:1 molar ratio) being preferred. Typically, the catalyst and alkyl alcohol are mixed together and dried using vacuum and heat (e.g., 100 mbar and 140 ℃) to form the alcohol catalyst. Typically, Ethylene Oxide (EO) is then slowly added to the dried alcohol catalyst. Typically, after EO is added to the dry alcohol catalyst, the pH of the reaction mixture is lowered, for example by using lactic acid. Typically, acetic acid is then added to neutralize the reaction to form the ethoxylated alkyl alcohol.

Typically, ethoxylated alkyl alcohols are treated with SO in a falling film reactor₃Sulfation to form a surfactant acid precursor, which is then neutralized with NaOH to form an ethoxylated alkyl sulfate anionic detersive surfactant (AES).

Generally, the molar ethoxylation profile of AES is manipulated by controlling the molar ethoxylation profile of the ethoxylated alcohol product during its synthesis. The catalyst used in the reaction is preferably a base having a pKb.ltoreq.5, more preferably having a pKb.ltoreq.3, more preferably having a pKb.ltoreq.1, most preferably having a pKb.ltoreq.0.5. Preferred catalysts are KOH and NaOH. In general, the choice of catalyst controls the molar ethoxylation distribution. In general, a stronger base catalyst will favor a broader molar ethoxylation distribution with a higher content of unethoxylated material and a higher content of ethoxylated material having a degree of ethoxylation of 2 or greater. In general, a weaker base catalyst will favor a narrower molar ethoxylation distribution, with a lower content of unethoxylated alcohol and a lower content of ethoxylated material having a degree of ethoxylation of 2 or more.

The molar ethoxylation distribution of AES is typically determined by measuring the molecular weight distribution via mass spectrometry.

Method for producing AES particles: typically, AES particles are made by an agglomeration process. Typically, the partially ethoxylated alkyl sulphate anionic detersive surfactant, salt and silica are dosed into one or more mixers and agglomerated to form AES particles.

Polymer particles: typically, the polymer particles comprise: (a)60 to 90 weight percent of the copolymer and (b)10 to 40 weight percent of the salt. Preferably, the copolymer comprises: (i) from 50 to less than 98 weight percent structural units derived from one or more monomers comprising a carboxyl group; (ii) from 1 wt% to less than 49 wt% structural units derived from one or more monomers comprising a sulfonate moiety; and (iii) from 1 to 49 wt% structural units derived from one or more types of monomers selected from ether bond-containing monomers represented by formulas (I) and (II):

formula (I):

wherein in formula (I), R₀Represents a hydrogen atom or CH₃Group, R represents CH₂Radical, CH₂CH₂A group, or a single bond, X represents a number from 0 to 5, with the proviso that when R is a single bond, X represents a number from 1 to 5, and R₁Is a hydrogen atom or C₁To C₂₀An organic group;

formula (II)

Wherein in formula (II), R₀Represents a hydrogen atom or CH₃Group, R represents CH₂Radical, CH₂CH₂A group or a single bond, X represents a number from 0 to 5, and R₁Is a hydrogen atom or C₁To C₂₀An organic group.

It may be preferred that the polymer has a weight average molecular weight of at least 50kDa or even at least 70 kDa.

Preferably, the salt is selected from sulphate and/or carbonate. Preferred salts are sulfates, more preferably sodium sulfate. Preferably, the polymer particles are spray-dried particles. Typically, the polymer particles have a bulk density of from 300g/l to 500 g/l. Typically, the polymer particles have a weight average particle size in the range of from 300 microns to 500 microns. Typically, the particle size distribution of the polymer particles is such that the geometric span is from 1.8 to 2.0.

Method for producing polymer particles: typically, the polymer particles are prepared by a spray drying process. Preferably, the polymer is contacted with water to form an aqueous polymer mixture. Preferably, the salt is then contacted with the aqueous polymer mixture to form a crutcher mixture. Preferably, the crutcher mixture comprises 60 to 80 wt% water. Preferably, the crutcher mixture is then spray dried to form the polymer particles. This sequence of addition ensures excellent dispersion of the polymer in the crutcher mixture, which in turn results in excellent drying characteristics and excellent physical properties of the polymer particles, such as excellent cake strength characteristics.

Toner particles: the particles comprise: (a)2 to 10 weight percent of a toner, wherein the toner has the following structure:

wherein: r1 and R2 are independently selected from: h; an alkyl group; an alkoxy group; an alkylene oxide; an alkyl terminated alkylene oxide; urea; and an amide group; r3 is substituted aryl; x is a substituent comprising a sulfonamide moiety and optionally an alkyl and/or aryl moiety, and wherein the substituent comprises at least one alkyleneoxy chain comprising an average molar distribution of at least four alkyleneoxy moieties; and (b)60 to 98 wt% clay. Preferably, the clay is a montmorillonite clay, also known as bentonite clay. Preferably, the particles comprise 90 to 98 wt% clay. It may also be preferred for the composition to comprise an inorganic salt, such as sodium sulphate, preferably 20 to 38% by weight sodium sulphate.

Method for producing toner particles: the toner particles may be prepared by an agglomeration process. Typically, the toner and clay are dosed into one or more agitators and agglomerated to form toner agglomerates.

Silicone particles: the silicone particles comprise: (a)10 to 20 wt% siloxane; and (b)50 to 80 wt.% of a carrier. The support may be a zeolite. The siloxane may be in the form of an agglomerate.

Method for producing silicone particles: the silicone particles can be prepared by an agglomeration process. Typically, the silicone and carrier are dosed into one or more mixers and agglomerated to form silicone agglomerates.

Detergent composition: generally, suitable laundry detergent compositions comprise a detergent ingredient selected from: detersive surfactants such as anionic detersive surfactants, nonionic detersive surfactants, cationic detersive surfactants, zwitterionic detersive surfactants, and amphoteric detersive surfactants; polymers such as carboxylate polymers, soil release polymers, anti-redeposition polymers, cellulosic polymers and care polymers; bleaching agents such as sources of hydrogen peroxide, bleach activators, bleach catalysts and preformed peracids; photobleaching, such as sulfonated zinc and/or aluminum phthalocyanines; enzymes such as proteases, amylases, cellulases, lipases; a zeolite builder; a phosphate builder; co-builders, such as citric acid and citrates; carbonates such as sodium carbonate and sodium bicarbonate; sulfates, such as sodium sulfate; silicates, such as sodium silicate; chloride salts, such as sodium chloride; a whitening agent; a chelating agent; a toner; a dye transfer inhibiting agent; dyeing processA material fixing agent; a fragrance; a siloxane; fabric softeners, such as clay; flocculants such as polyethylene oxide; a suds suppressor; and any combination thereof.

Detersive surfactant: suitable detersive surfactants include anionic detersive surfactants, nonionic detersive surfactants, cationic detersive surfactants, zwitterionic detersive surfactants, and amphoteric detersive surfactants. Suitable detersive surfactants can be linear or branched, substituted or unsubstituted, and can be derived from petrochemical or biological materials.

Anionic detersive surfactant: suitable anionic detersive surfactants include sulphonate and sulphate detersive surfactants.

Suitable sulphonate detersive surfactants include methyl ester sulphonate, α -olefin sulphonate, alkyl benzene sulphonate, especially alkyl benzene sulphonate, preferably C_10-13An alkylbenzene sulfonate. Suitable alkyl benzene sulfonates (LAS) are available, preferably obtained by sulfonating commercially available Linear Alkyl Benzenes (LAB); suitable LAB include low 2-phenyl LAB, other suitable LAB include high 2-phenyl LAB, such as that sold under the trade name Sasol

Those provided.

Suitable sulphate detersive surfactants include alkyl sulphates, preferably C_8-18Alkyl sulfates, or predominantly C₁₂An alkyl sulfate.

Preferred sulphate detersive surfactants are alkyl alkoxylated sulphates, preferably alkyl ethoxylated sulphates, preferably C_8-18Alkyl alkoxylated sulfates, preferably, C_8-18Alkyl ethoxylated sulphate, preferably having an average degree of alkoxylation of from 0.5 to 20, preferably from 0.5 to 10, preferably the alkyl alkoxylated sulphate is C_8-18Alkyl ethoxylated sulfates having from 0.5 to 10, preferably, 0.5 to 5, more preferably, 0.5 to 3, and most preferably, 0.5 to 31.5 average degree of ethoxylation.

Alkyl sulfates, alkyl alkoxylated sulfates and alkyl benzene sulfonates may be linear or branched, substituted or unsubstituted, and may be derived from petrochemical or biological materials.

Other suitable anionic detersive surfactants include alkyl ether carboxylates.

Suitable anionic detersive surfactants may be in the form of salts, and suitable counterions include sodium, calcium, magnesium, amino alcohols, and any combination thereof. The preferred counterion is sodium.

Nonionic detersive surfactant: suitable nonionic detersive surfactants are selected from: c₈-C₁₈Alkyl ethoxylates, such as those from Shell

A nonionic surfactant; c₆-C₁₂Alkylphenol alkoxylates, wherein preferably the alkoxylate units are ethylene oxide units, propylene oxide units, or mixtures thereof; c₁₂-C₁₈Alcohol and C₆-C₁₂Condensates of alkylphenols with ethyleneoxy/propyleneoxy block polymers, such as those from BASF

Alkyl polysaccharides, preferably alkyl polyglycosides; a methyl ester ethoxylate; polyhydroxy fatty acid amides; ether-terminated poly (alkoxylated) alcohol surfactants; and mixtures thereof.

Suitable nonionic detersive surfactants are alkyl polyglucosides and/or alkyl alkoxylated alcohols.

Suitable nonionic detersive surfactants include alkyl alkoxylated alcohols, preferably C_8-18Alkyl alkoxylated alcohols, preferably C_8-18An alkyl ethoxylated alcohol, preferably said alkyl alkoxylated alcohol having an average degree of alkoxylation of from 1 to 50, preferably from 1 to 30, or from 1 to 20, or from 1 to 10, preferably said alkyl alkoxylated alcohol is C_8-18Alkyl ethoxylated alcohols havingAn average degree of ethoxylation of from 1 to 10, preferably from 1 to 7, more preferably from 1 to 5, and most preferably from 3 to 7. The alkyl alkoxylated alcohol may be linear or branched, and substituted or unsubstituted.

Suitable nonionic detersive surfactants include secondary alcohol-based detersive surfactants.

Cationic detersive surfactant: suitable cationic detersive surfactants include alkyl pyridinium compounds, alkyl quaternary ammonium compounds, alkyl quaternary phosphonium compounds, alkyl tertiary sulfonium compounds, and mixtures thereof.

Preferred cationic detersive surfactants are quaternary ammonium compounds having the general formula:

(R)(R₁)(R₂)(R₃)N⁺X^-

wherein R is a linear or branched, substituted or unsubstituted C_6-18Alkyl or alkenyl moieties, R₁And R₂Independently selected from methyl or ethyl moieties, R₃Is a hydroxyl, hydroxymethyl or hydroxyethyl moiety, X is an anion that provides electrical neutrality, preferred anions include: halide, preferably chloride; sulfate radical; and a sulfonate group.

Zwitterionic detersive surfactant: suitable zwitterionic detersive surfactants include amine oxides and/or betaines.

Polymer and method of making same: suitable polymers include carboxylate polymers, soil release polymers, anti-redeposition polymers, cellulosic polymers, care polymers, and any combination thereof.

Carboxylate polymer: the composition may comprise a carboxylate polymer, such as a maleate/acrylate random copolymer or a polyacrylate homopolymer. Suitable carboxylate polymers include: a polyacrylate homopolymer having a molecular weight of 4,000Da to 9,000 Da; a maleate/acrylate random copolymer having a molecular weight of from 50,000Da to 100,000Da, or from 60,000Da to 80,000 Da.

Another suitable carboxylate polymer is a copolymer comprising: (i) from 50 to less than 98 weight percent structural units derived from one or more monomers comprising a carboxyl group; (ii) from 1 wt% to less than 49 wt% structural units derived from one or more monomers comprising a sulfonate moiety; and (iii) from 1 to 49 wt% structural units derived from one or more types of monomers selected from ether bond-containing monomers represented by formulas (I) and (II):

formula (I):

formula (II)

Soil release polymers: the composition may comprise a soil release polymer. Suitable soil release polymers have a structure as defined by one of the following structures (I), (II), or (III):

(I) -[(OCHR¹-CHR²)_a-O-OC-Ar-CO-]_d

(II) [(OCHR³-CHR⁴)_b-O-OC-sAr-CO-]_e

(III) -[(OCHR⁵-CHR⁶)_c-OR⁷]_f

wherein:

a. b and c are 1 to 200;

d. e and f are 1 to 50;

ar is 1, 4-substituted phenylene;

sAr is SO substituted in the 5-position₃1, 3-substituted phenylene substituted with Me;

me is Li, K, Mg/2, Ca/2, Al/3, ammonium, monoalkylammonium, dialkylammonium, trialkylammonium or tetraalkylammonium, where the alkyl radical is C₁-C₁₈Alkyl or C₂-C₁₀Hydroxyalkyl, or mixtures thereof;

R¹、R²、R³、R⁴、R⁵and R⁶Independently selected from H or C₁-C₁₈N-alkyl or C₁-C₁₈An isoalkyl group; and is

R⁷Is straight-chain or branched C₁-C₁₈Alkyl, or straight or branched C₂-C₃₀Alkenyl, or cycloalkyl having 5 to 9 carbon atoms, or C₈-C₃₀Aryl radicals, or C₆-C₃₀An aralkyl group.

Suitable soil release polymers are prepared from Clariant and

a range of polymers are sold, for example,

SRN240 and

SRA 300. Other suitable soil release polymers are prepared from Solvay and

a range of polymers are sold, for example,

SF2 and

Crystal。

anti-redeposition polymers: suitable anti-redeposition polymers include polyethylene glycol polymers and/or polyethyleneimine polymers.

Suitable polyethylene glycol polymers include random graft copolymers comprising: (i) a hydrophilic backbone comprising polyethylene glycol; and (ii) one or more hydrophobic side chains selected from the group consisting of: c₄-C₂₅Alkyl radical, polypropylene, polybutylene, saturated C₁-C₆Vinyl esters of monocarboxylic acids, C of acrylic or methacrylic acid₁-C₆Alkyl esters, and mixtures thereof. Suitable polyethylene glycol polymers have a polyethylene glycol backbone with randomly grafted polyvinyl acetate side chains. The average molecular weight of the polyethylene glycol backbone may be in the range of 2,000Da to 20,000Da, or 4,000Da to 8,000 Da. The molecular weight ratio of the polyethylene glycol backbone to the polyvinyl acetate side chains can be from 1:1 to 1:5, or from 1:1.2 to 1: 2. The average number of grafting sites per ethylene oxide unit may be less than 1, or less than 0.8, the average number of grafting sites per ethylene oxide unit may be in the range of 0.5 to 0.9, or the average number of grafting sites per ethylene oxide unit may be in the range of 0.1 to 0.5, or 0.2 to 0.4. A suitable polyethylene glycol polymer is Sokalan HP 22. Suitable polyethylene glycol polymers are described in WO 08/007320.

Cellulose polymers: suitable cellulosic polymers are selected from the group consisting of alkyl celluloses, alkylalkoxy alkyl celluloses, carboxyalkyl celluloses, alkylcarboxyalkyl celluloses, sulfoalkyl celluloses, more preferably from the group consisting of carboxymethyl cellulose, methyl hydroxyethyl cellulose, methyl carboxymethyl cellulose and mixtures thereof.

Suitable carboxymethyl celluloses have a degree of carboxymethyl substitution of from 0.5 to 0.9 and a molecular weight of from 100,000Da to 300,000 Da.

Suitable carboxymethyl celluloses have a degree of substitution greater than 0.65 and a degree of blockiness greater than 0.45, for example as described in WO 09/154933.

Care polymers: suitable care polymers include cationically modified or hydrophobically modified cellulosic polymers. Such modified cellulosic polymers can provide anti-abrasion benefits and dye lock benefits to fabrics during the wash cycle. Suitable cellulosic polymers include cationically modified hydroxyethyl cellulose.

Other suitable care polymers include dye-locking polymers such as condensation oligomers produced by condensation of imidazole and epichlorohydrin, preferably in a 1:4:1 ratio. Suitable commercially available dye-locking polymers are

FDI(Cognis)。

Other suitable care polymers include aminosilicones, which provide fabric feel benefits and fabric shape retention benefits.

Bleaching agent: suitable bleaching agents include sources of hydrogen peroxide, bleach activators, bleach catalysts, preformed peracids, and any combination thereof. Particularly suitable bleaching agents include a source of hydrogen peroxide in combination with a bleach activator and/or bleach catalyst.

Hydrogen peroxide source: suitable sources of hydrogen peroxide include sodium perborate and/or sodium percarbonate.

Bleach activators: suitable bleach activators include tetraacetylethylenediamine and/or alkylphenol sulfonates.

Bleaching catalyst: the composition may comprise a bleach catalyst. Suitable bleach catalysts include the peroxyimine cation bleach catalysts, transition metal bleach catalysts, especially manganese and iron ion bleach catalysts. Suitable bleach catalysts have a structure corresponding to the general formula:

wherein R is¹³Selected from: 2-ethylhexyl group, 2-propylheptyl group, 2-butyloctyl group, 2-pentylnonyl group, 2-hexyldecyl group, n-dodecyl group, n-tetradecyl group, n-hexadecyl group, n-octadecyl group, isononyl group, isodecyl group, isotridecyl group, and isopentadecyl group.

Preformed peracids: suitable preformed peracids include phthalimido-peroxycaproic acid.

Enzyme: suitable enzymes include lipases, proteases, cellulases, amylases, and any combination thereof.

Protease enzyme: suitable proteases include metalloproteases and serine proteases. Examples of suitable neutral or alkaline proteases include: subtilisin (EC 3.4.21.62); a trypsin-type or chymotrypsin-type protease; and a metalloprotease. Suitable proteases include chemically or genetically modified mutants of the aforementioned suitable proteases.

Suitable commercially available proteases include those under the trade name

Savinase

And

those sold by Novozymes A/S (Denmark); under the trade name of

Preferenz

A series of proteases comprising

P280、

P281、

P2018-C、

P2081-WE、

P2082-EE and

P2083-A/J、

Purafect

Purafect

and Purafect

Those sold by DuPont; under the trade name of

And

those sold by Solvay Enzymes; those from Henkel/Kemira, BLAP (sequence shown in FIG. 29 of US 5,352,604, with the following mutations)The variant S99D + S101R + S103A + V104I + G159S, hereinafter referred to as BLAP); BLAP R (BLAP with S3T + V4I + V199M + V205I + L217D), BLAP X (BLAP with S3T + V4I + V205I), and BLAP F49 (BLAP with S3T + V4I + A194P + V199M + V205I + L217D), all from Henkel/Kemira; and KAP from Kao (alkalophilic bacillus subtilisin with mutations a230V + S256G + S259N).

Suitable proteases are described in WO11/140316 and WO 11/072117.

AmylaseSuitable amylases are derived from AA560 α amylase endogenously derived from Bacillus DSM 12649, preferably with the following mutations R118K, D183, G184, N195F, R320K, and/or R458K

Plus、Natalase、

Ultra、

SZ、

(both from Novozymes) and

AA，Preferenz

a series of amylase enzymes are provided,

and

Ox Am，

HT Plus (both from Du Pont).

Suitable amylases are described in WO 06/002643.

Cellulase enzymes: suitable cellulases include those of bacterial or fungal origin. Chemically modified or protein engineered mutants are also suitable. Suitable cellulases include cellulases from bacillus, pseudomonas, humicola, fusarium, rhizopus, acremonium, such as fungal cellulases produced by humicola insolens, myceliophthora thermophila, and fusarium oxysporum.

Commercially available cellulases include

And

Premium，

and

(Novozymes A/S)、

the series of enzymes (DuPont), and

series of Enzymes (AB Enzymes). Suitable commercially available cellulases include

Premium、

Classic. Suitable proteases are described in WO07/144857 and WO 10/056652.

Lipase enzyme: suitable lipases include those of bacterial, fungal or synthetic origin, and variants thereof.Chemically modified or protein engineered mutants are also suitable. Examples of suitable lipases include lipases from Humicola (Humicola), the synonym Thermomyces (Thermomyces), such as Humicola lanuginosa (h.lanuginosa), Thermomyces lanuginosus (t.lanuginosus).

The lipase may be a "first cycle lipase", for example, such as those described in WO06/090335 and WO 13/116261. In one aspect, the lipase is a first wash lipase, preferably a variant of a wild-type lipase from thermomyces lanuginosus comprising a T231R and/or N233R mutation. Preferred lipases include those known under the trade name

And

those sold by Novozymes (Bagsvaerd, Denmark).

Other suitable lipases include: liprl 139, e.g., as described in WO 2013/171241; and TfuLip 2; for example as described in WO2011/084412 and WO 2013/033318.

Other enzymes: other suitable enzymes are bleaching enzymes such as peroxidases/oxidases, including those of plant, bacterial or fungal origin and variants thereof. Commercially available peroxidases include

(Novozymes A/S). Other suitable enzymes include choline oxidase and perhydrolase, such as for Gentle Power Bleach^TMOf (a).

Other suitable enzymes include those available under the trade name

(from Novozymes A/S, Bagsvaerd, Denmark) and

pectate lyases sold by DuPont and commercial suppliersName of article

(Novozymes A/S, Bagsvaerd, Denmark) and

mannanase sold by (Du Pont).

Zeolite builders: the composition may comprise a zeolite builder. The composition may comprise from 0 wt% to 5 wt% zeolite builder, or 3 wt% zeolite builder. The composition may even be substantially free of zeolite builder; substantially free means "not intentionally added". Typical zeolite builders include zeolite a, zeolite P and zeolite MAP.

Phosphate builders: the composition may comprise a phosphate builder. The composition may comprise from 0 wt% to 5 wt% phosphate builder, or to 3 wt% phosphate builder. The composition may even be substantially free of phosphate builder; substantially free means "not intentionally added". A typical phosphate builder is sodium tripolyphosphate.

Carbonate salt: the composition may comprise a carbonate salt. The composition may comprise from 0 wt% to 10 wt% carbonate, or to 5 wt% carbonate. The composition may even be substantially free of carbonate; substantially free means "not intentionally added". Suitable carbonates include sodium carbonate and sodium bicarbonate;

silicates of acid or alkali: the composition may comprise a silicate. The composition may comprise from 0 wt% to 10 wt% silicate, or to 5 wt% silicate. The preferred silicate is sodium silicate, particularly preferred is Na having a value of 1.0 to 2.8, preferably 1.6 to 2.0₂O:SiO₂Sodium silicate in a ratio.

Sulfates of sulfuric acid: a suitable sulphate is sodium sulphate.

Whitening agent: suitable optical brighteners include: distyrylbiphenyl compounds, e.g.

CBS-X, diaminostilbene disulfonic acid compounds, e.g.

DMS pure Xtra and

HRH, and pyrazoline compounds, e.g.

SN and coumarin compounds, e.g.

SWN。

Preferred brighteners are sodium 2- (4-styryl-3-sulfophenyl) -2H-naphthol [1,2-d ] triazole, 4' -bis { [ (4-phenylamino-6- (N-methyl-N-2-hydroxyethyl) amino-1, 3, 5-triazin-2-yl) ], disodium amino } stilbene-2-2 ' -disulfonate, disodium 4,4' -bis { [ (4-phenylamino-6-morpholino-1, 3, 5-triazin-2-yl) ] amino } stilbene-2-2 ' -disulfonate, and disodium 4,4' -bis (2-sulfostyryl) biphenyl, suitable fluorescent whitening agents are C.I. fluorescent whitening agents 260, which can be used in their β or α -crystal form or in mixtures of these crystal forms.

Chelating agents: the composition may further comprise a chelating agent selected from: diethylene triamine pentaacetate, diethylene triamine penta (methyl phosphonic acid), ethylene diamine-N' -disuccinic acid, ethylene diamine tetraacetate, ethylene diamine tetra (methylene phosphonic acid), and hydroxyethane di (methylene phosphonic acid). Preferred chelating agents are ethylenediamine-N' -disuccinic acid (EDDS) and/or hydroxyethane diphosphonic acid (HEDP). The composition preferably comprises ethylenediamine-N' -disuccinic acid or salts thereof. Preferably the ethylenediamine-N' -disuccinic acid is in the form of the S, S enantiomer. Preferably, the composition comprises 4, 5-dihydroxyisophthalate disodium salt. Preferred chelating agents may also act as calcium carbonate crystal growth inhibitors, such as: 1-hydroxyethane diphosphonic acid (HEDP) and salts thereof; n, N-dicarboxymethyl-2-aminopentane-1, 5-dioic acid or its salt, 2-phosphonobutane-1,2, 4-tricarboxylic acids and salts thereof; and combinations thereof.

Toner and image forming apparatus: suitable hueing agents include small molecule dyes, typically of the acid, direct, basic, reactive (including their hydrolyzed forms) or solvent or disperse dye color index (c.i.) classes, such as dyes classified as blue, violet, red, green or black, and provide the desired hue, either alone or in combination. Preferably, such toners include acid violet 50, direct violet 9, 66 and 99, solvent violet 13 and any combination thereof.

Many toners suitable for use in the present invention are known and described in the art, such as the toners described in WO 2014/089386.

Suitable hueing agents include phthalocyanine and azo dye conjugates, such as described in WO 2009/069077.

Suitable toners may be alkoxylated. Such alkoxylated compounds may be prepared by organic synthesis, which may result in a mixture of molecules having different degrees of alkoxylation. Such mixtures may be used directly to provide a toner, or may be subjected to a purification step to increase the proportion of target molecules. Suitable hueing agents include alkoxylated disazo dyes, such as described in WO2012/054835, and/or alkoxylated thiophene azo dyes, such as described in WO2008/087497 and WO 2012/166768.

The hueing agent may be incorporated into the detergent composition as part of the reaction mixture that is the result of the organic synthesis of the dye molecule with one or more optional purification steps. Such reaction mixtures generally comprise the dye molecules themselves and may, in addition, comprise unreacted starting materials and/or by-products of organic synthesis routes. Suitable hueing agents may be incorporated into the hueing dye particles, such as described in WO 2009/069077.

Dye transfer inhibitors: suitable dye transfer inhibiting agents include polyamine N-oxide polymers, copolymers of N-vinylpyrrolidone and N-vinylimidazole, polyvinylpyrrolidone, polyvinyloxazolidone, polyvinylimidazole, and mixtures thereof. Preferred are poly (vinylpyrrolidone),Poly (vinylpyridine betaine), poly (vinylpyridine N-oxide), poly (vinylpyrrolidone-vinylimidazole) and mixtures thereof. Suitable commercially available dye transfer inhibitors include PVP-K15 and K30(Ashland),

HP165、HP50、HP53、HP59、HP56K、HP56、HP66(BASF)，

s-400, S403E, and S-100 (Ashland).

Perfume: suitable perfumes comprise perfume materials selected from the group consisting of: (a) a perfume material having a ClogP of less than 3.0 and a boiling point of less than 250 ℃ (quadrant 1 perfume material); (b) perfume materials having a ClogP of less than 3.0 and a boiling point of 250 ℃ or higher (quadrant 2 perfume materials); (c) a perfume material having a ClogP of 3.0 or greater and a boiling point of less than 250 ℃ (quadrant 3 perfume material); (d) a perfume material having a ClogP of 3.0 or greater and a boiling point of 250 ℃ or higher (quadrant 4 perfume material); and (e) mixtures thereof.

It may be preferred for the perfume to be in the form of a perfume delivery technology. Such delivery techniques are also stable and enhance deposition and release of perfume materials from laundered fabrics. Such perfume delivery technologies can also be used to further increase the longevity of perfume release from laundered fabrics. Suitable perfume delivery technologies include: perfume microcapsules, pro-perfumes, polymer assisted delivery, molecular assisted delivery, fiber assisted delivery, amine assisted delivery, cyclodextrins, starch encapsulating complexes, zeolites and other inorganic carriers and any mixtures thereof. Suitable perfume microcapsules are described in WO 2009/101593.

Siloxanes: suitable silicones include polydimethylsiloxane and aminosilicone. Suitable siloxanes are described in WO 05075616.

Process for preparing solid compositions: in general, the particles of the composition may be prepared by any suitable method. For example, spray drying, agglomeration, extrusion and any of themAnd (4) combining.

Generally, a suitable spray drying process comprises the steps of forming an aqueous slurry mixture, transferring it to a pressure nozzle by means of at least one pump, preferably two pumps. Atomizing the aqueous slurry mixture into a spray drying tower and drying the aqueous slurry mixture to form spray dried particles. Preferably, the spray drying tower is a counter current spray drying tower, although a co current spray drying tower may also be suitable.

Typically, the spray-dried powder is subjected to cooling, e.g. stripping. Typically, the spray-dried powder is subjected to particle size classification, e.g. sieving, to obtain the desired particle size distribution. Preferably, the spray-dried powder has a particle size distribution such that the weight average particle size is in the range of 300 microns to 500 microns, and less than 10% by weight of the spray-dried particles have a particle size greater than 2360 microns.

It may be preferred to heat the aqueous slurry mixture to raise the temperature prior to atomization into a spray drying tower, such as described in WO 2009/158162.

It may be preferred that an anionic surfactant such as linear alkyl benzene sulphonate is introduced into the spray drying process after the step of forming the aqueous slurry mixture: for example, after pumping, an acid precursor is introduced into the aqueous slurry mixture, such as described in WO 09/158449.

It may be preferred that a gas such as air is introduced into the spray drying process after the step of forming the aqueous slurry, such as described in WO 2013/181205.

It may be preferred that any inorganic ingredients such as sodium sulphate and sodium carbonate, if present in the aqueous slurry mixture, are micronized to small particle sizes, such as described in WO 2012/134969.

Generally, a suitable agglomeration process comprises the step of contacting a detersive ingredient, such as a detersive surfactant, for example linear alkyl benzene sulphonate (LAS) and/or alkyl alkoxylated sulphate, with an inorganic material, such as sodium carbonate and/or silica, in a mixer. The agglomeration process may also be an in-situ neutralisation agglomeration process wherein an acidic precursor of a detersive surfactant, such as LAS, is contacted with a basic material, such as carbonate and/or sodium hydroxide, in a mixer, and wherein the acidic precursor of the detersive surfactant is neutralised by the basic material during the agglomeration process to form the detersive surfactant.

Other suitable detergent ingredients that may be agglomerated include polymers, chelants, bleach activators, silicones, and any combination thereof.

The agglomeration process may be a high, medium, or low shear agglomeration process, wherein a high shear, medium shear, or low shear mixer is used, respectively. The agglomeration process may be a multi-step agglomeration process in which two or more agitators are used, such as a combination of a high shear agitator and a medium or low shear agitator. The agglomeration process may be a continuous process or a batch process.

It may be preferred for the agglomerates to be subjected to a drying step, for example, a fluid bed drying step. It may also be preferred for the agglomerates to be subjected to a cooling step, for example, a fluidized bed cooling step.

Typically, the agglomerates are subjected to particle size classification, e.g., fluidized bed elution and/or sieving, to obtain the desired particle size distribution. Preferably, the agglomerates have a particle size distribution such that the weight average particle size is in the range of 300 microns to 800 microns, and less than 10% by weight of the agglomerates have a particle size of less than 150 microns, and less than 10% by weight of the agglomerates have a particle size of greater than 1200 microns.

It may be preferred for fine and oversized agglomerates to be recycled back into the agglomeration process. Typically, the oversized particles are subjected to a size reduction step, such as milling, and recycled back to an appropriate location in the agglomeration process, such as an agitator. Typically, the fines are recycled back to an appropriate location in the agglomeration process, such as an agitator.

It may be preferred for ingredients such as polymer and/or nonionic detersive surfactant and/or perfume to be sprayed onto base detergent particles, such as spray-dried base detergent particles and/or agglomerated base detergent particles. Typically, this spraying step is carried out in a tumble drum mixer.

Washing fabricMethod (2): a method of laundering fabrics comprises the steps of contacting a solid composition with water to form a wash liquor, and laundering fabrics in said wash liquor. Typically, the wash liquor has a temperature of from above 0 ℃ to 90 ℃, or to 60 ℃, or to 40 ℃, or to 30 ℃, or to 20 ℃. The fabric may be contacted with water before, after, or simultaneously with contacting the solid composition with water. Typically, the wash liquor is formed by contacting the laundry detergent with water in such an amount that the concentration of the laundry detergent composition in the wash liquor is from 0.2g/l to 20g/l, or from 0.5g/l to 10g/l, or to 5.0 g/l. The method of washing fabrics may be carried out in a front loading automatic washing machine, a top loading automatic washing machine, including high efficiency automatic washing machines, or a suitable hand washing receptacle. Typically, the wash liquor comprises 90 litres or less, or 60 litres or less, or 15 litres or less, or 10 litres or less of water. Typically, 200g or less, or 150g or less, or 100g or less, or 50g or less of the laundry detergent composition is contacted with water to form the wash liquor.

Dimension line: the dimensions and values disclosed herein are not to be understood as being strictly limited to the exact numerical values recited. Rather, unless otherwise specified, each such dimension is intended to mean both the recited value and a functionally equivalent range surrounding that value. For example, a dimension disclosed as "40 mm" is intended to mean "about 40 mm".

Literature reference: each document cited herein, including any cross-referenced or related patent or patent application and any patent application or patent to which this application claims priority or its benefits, is hereby incorporated by reference in its entirety unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with respect to any invention disclosed or claimed herein or that it alone, or in combination with any other reference or references, teaches, suggests or discloses any such invention. Further, to the extent that any meaning or definition of a term in this document conflicts with any meaning or definition of the same term in a document incorporated by reference, the same term in this document shall governMean or definition of.

Detailed description of the preferred embodiments: while particular embodiments of the present invention have been illustrated and described, it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention. It is therefore intended to cover in the appended claims all such changes and modifications that are within the scope of this invention.

Examples

Example 1: the following samples were prepared by the methods described below. Sample 3 is in accordance with the present invention. Sample 1 is a comparative sample with no toner particles present, and sample 2 is a comparative sample with no AES particles present.

Detergents supplied by Equest-commercially available

Particle 1: toner particles and method for producing the same：

501.8g of sodium bentonite (SPV 200) powder substrate (provided by MTI) was weighed into the bowl of a food blender (Philips HR 7626). The lid of the stirrer was locked in place and the parafilm was stretched to cover the inlet. 19.8g of liquid toner was weighed in a syringe and perforated on a paraffin film to pass the syringe. The agitator was switched to maximum speed and toner was added via syringe stepwise. Once all the toner was added, it was allowed to stir for 2 minutes. The stirrer was turned off, any agglomerated material on the blades scraped back into the stirrer, and then stirred for an additional 2 minutes to produce the final material.

Toner particle composition：

Particle 2: AES particles: the following AES particles were prepared by agglomeration.

Composition (I)	By weight%
		AES¹	46.3
Sodium carbonate	33.3
		Silicon dioxide	14.3
Moisture content&Miscellaneous items	6.1

1-partially ethoxylated alkyl sulphate anionic detersive surfactant having a molar average degree of ethoxylation of 1.0 and having a molar ethoxylation distribution such that:

(i)45 wt.% is unethoxylated, having a degree of ethoxylation of 0;

(ii)24 wt% has a degree of ethoxylation of 1; and

(iii)31 wt% has a degree of ethoxylation of 2 or greater.

Example 2: washing and whiteness measuring method: samples 1,2 and 3 above were added individually to the drawers of 4 independent Miele1714 front loading washing machines (each sample was repeated 4 times). The washing machine was set to 40 ℃ and short cotton cycle (1.25 hours). Hard water (23.1Clark, 131.9ppm) was used. The soil was placed into the drum of the washing machine (20g AS1 (explained below), 17g Sigma Aldrich yeast) on top of which ballast and whitening tracer were placed. Each load contained 10 terry cloths 20X 20cm (2 rib plaits for single ply)Minor cycle analysis, 8 strips for multiple (4 rib plaits)). The total weight of load (white tracer and low cotton ballast) is equal to 3 Kg. The fabric was then analyzed for single and multiple cycles to measure dye deposition on the fabric.

Whiteness analysis: each fabric was analyzed using a polaroris Spectrophotometer to assess the deposition of dye on each fabric. In the absence of AES particles (sample 2), statistically significant toner enhancement occurred on the fabric over multiple wash cycles (difference b of-0.55 between multiple and single cycles). In the presence of AES particles (sample 3), no statistically significant toner enhancement occurred on the fabric over multiple cycles (difference b of-0.35 between multiple and single cycles).

Conclusion: sample 3 exhibited a lower multi-cycle toner accumulation characteristic relative to sample 2.

Example 3: exemplary embodiments of free-flowing solid particulate laundry detergent compositions：

The above-described exemplary embodiments of a free-flowing solid particulate laundry detergent may be prepared such that the particle architecture of the detergent comprises:

granules	By weight%
		AES particles	0.5 to 20 percent
Silicone particles	0.1 to 5 percent
		Spray-dried particles	35 to 80 percent
LAS particles	1 to 30 percent
		Toning particles	0.1 to 5 percent
Polymer particles	0.1 to 5 percent

Claims

1. A free-flowing solid particulate laundry detergent composition comprising:

(a)0.1 to 5 wt% of toner particles comprising:

(i)2 to 10 weight percent of a toner, wherein the toner has the following structure:

wherein:

R₁and R₂Independently selected from: h; an alkyl group; an alkoxy group; an alkylene oxide;an alkyl terminated alkylene oxide; urea; and an amide group;

R₃is a substituted aryl group;

(ii)60 to 98 weight percent of a clay; and

(b)0.5 to 20% by weight of AES particles comprising:

(i) from 40 wt% to 60 wt% of a partially ethoxylated alkyl sulphate anionic detersive surfactant, wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has an average molar ethoxylation degree of from 0.8 to 1.2, and wherein the partially ethoxylated alkyl sulphate anionic detersive surfactant has a molar ethoxylation distribution such that:

(i.i)40 to 50 wt% are unethoxylated, having a degree of ethoxylation of 0;

(i.ii)20 to 30 wt% have a degree of ethoxylation of 1;

(i.iii)20 to 40 wt% have a degree of ethoxylation of 2 or more;

(ii)20 to 50 wt% of a salt, wherein the salt is selected from sulphate and/or carbonate; and

(iii)10 to 30% by weight of silica.

2. The composition of claim 1, wherein the composition comprises from 35% to 80% by weight of spray-dried particles comprising:

(a) from 8% to 24% by weight of alkyl benzene sulphonate anionic detersive surfactant;

(b)5 to 18 wt% of a silicate;

(c)0 to 10% by weight of sodium carbonate; and

(d)0 to 5% by weight of a carboxylate polymer.

3. The composition of any one of the preceding claims, wherein the composition comprises from 1 wt% to 30 wt% LAS particles comprising:

(a) from 30% to 50% by weight of an alkylbenzene sulphonate anionic detersive surfactant; and

(b)50 to 70 wt% of a salt, wherein the salt is a sodium salt and/or a carbonate salt.

4. The composition of claim 1, wherein the composition comprises from 0.1 to 5 wt% of polymer particles comprising:

(a) from 70 wt% to 90 wt% of a copolymer, wherein the copolymer comprises:

(i) from 50 to less than 98 weight percent structural units derived from one or more monomers comprising a carboxyl group;

(ii) from 1 wt% to less than 49 wt% structural units derived from one or more monomers comprising a sulfonate moiety; and

(iii) from 1 to 49 wt% structural units derived from one or more types of monomers selected from ether bond-containing monomers represented by formulas (I) and (II):

formula (I):

wherein in formula (I), R₀Represents a hydrogen atom or CH₃Group, R represents CH₂Radical, CH₂CH₂A group or a single bond, X represents a number from 0 to 5, with the proviso that when R is a single bond, X represents a number from 1 to 5, and R₁Is a hydrogen atom or C₁To C₂₀An organic group;

formula (II)

Wherein in formula (II), R₀Represents a hydrogen atom or CH₃Group, R represents CH₂Radical, CH₂CH₂A group or a single bond, X represents a number from 0 to 5, and R₁Is a hydrogen atom or C₁To C₂₀An organic group; and

(b)10 to 30 wt% of a salt, wherein the salt is selected from sulphate and/or carbonate.

5. The composition of claim 1, wherein the composition comprises from 0.1% to 5% by weight of silicone particles comprising:

(a)10 to 20 wt% of a siloxane; and

(b)50 to 80% by weight of a carrier.

6. The composition of claim 1, wherein the composition comprises:

(a) from 0 wt% to 5 wt% zeolite builder;

(b)0 to 5 wt% of a phosphate builder; and

(c)0 to 5% by weight of sodium carbonate.

7. The composition of claim 1 wherein the toner particles comprise montmorillonite clay.

8. The composition according to claim 1, wherein the AES particle comprises 20 to 50 wt% sodium sulfate.

9. A composition according to claim 1, wherein the weight ratio of partially ethoxylated alkyl sulphate anionic detersive surfactant to silica present in the AES particle is in the range 2:1 to 5: 1.